US3655635A - Tall oil rosin of low sulfur content - Google Patents

Tall oil rosin of low sulfur content Download PDF

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Publication number
US3655635A
US3655635A US794762*A US3655635DA US3655635A US 3655635 A US3655635 A US 3655635A US 3655635D A US3655635D A US 3655635DA US 3655635 A US3655635 A US 3655635A
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tall oil
parts
sulfur
oil rosin
rosin
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US794762*A
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Thomas F Sanderson
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Hercules LLC
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Hercules LLC
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    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
    • C09F1/00—Obtaining purification, or chemical modification of natural resins, e.g. oleo-resins
    • C09F1/02—Purification

Definitions

  • This invention relates to tall oil rosin containing relatively small amounts of sulfur compound impurities and tothe method of obtaining same.
  • Tall oil a by-product recovered from pine wood black liquor of the sulfate paper process, is comprised of rosin acids, fatty acids, certain amounts of unsaponifiable material, and trace amounts of sulfur-containing compounds.
  • a representative tall oil rosin is one comprised of, by weight, about 43% rosin acids (also referred to in the art as resin acids), about 41% fatty acids, about 16% unsaponifiable material and trace amounts of sulfur-containing compounds.
  • Fractional distillation of tall oil yields a fraction rich in fatty acids, and a fraction rich in rosin acids.
  • the fraction rich in rosin acids is often referred to in the art as tall oil rosin, and will contain small amounts of fatty acids and trace amounts of sulfur-containing compounds.
  • the amount of sulfur present in the sulfur-containing compounds will usually be, by weight, at least about 300 parts per million (p.p.m.) parts of tall oil rosin and higher.
  • the presence of such amounts of sulfur renders the attempted hydrogenation of tall oil rosin uneconomical in that the sulfur poisons hydrogenation catalysts, such as the noble metals, and renders them ineffective for their intended purpose.
  • the tall oil rosin employed in carrying out this invention will be comprised of fatty acids and sulfur-containing compounds, the amount of sulfur present therein being from about 300 to about 600 parts per million (p.p.m.) parts of tall oil rosin.
  • the fatty acids content will be less than about 10% by weight.
  • a solution is prepared by dissolving, by weight, from about 25 parts to about 67 parts of the tall oil rosin in about 75 parts to about 33 parts of a polar solvent. If required, the solvent can be heated to accomplish substantially complete dissolution of the tall oil rosin. The solution is subsequently cooled at least to a temperature at which the rosin acids will crystallize out. Crystallization is permitted to continue until the desired amount of rosin acids has precipitated. The crystals can be recovered in any convenient Patented Apr. 11, 1972 manner as by decantation, centrifugation, filtration, or the like. The recovered crystals can be washed to remove adhering impurities, if desired. Polar solvents, such as those specifically disclosed herein, are recommended for the washing step.
  • the polar solvent employed will be liquid under room temperature conditions. Polar solvents that are liquid at temperatures as low as about -40 C. can be satisfactorily employed. Suitable polar solvents for use in carrying out this invention include acetone, methyl ethyl ketone, ethyl acetate, ethyl alcohol, methyl isobutyl ketone, isopropyl alcohol, diethylene glycol diethyl ether (diethyl Carbitol), diethylene glycol dimethyl ether (dimethyl Carbitol), and Z-methoxyethanol (methyl Cellosolve). Mixtures of two or more polar solvents can be employed if desired.
  • Washed crystals are placed in an oven maintained at a temperature of about C. and dried. About 41.5 parts of tall oil rosin crystals are obtained which still contain trace amounts of sulfur-containing compounds; however, the amount thereof has been reduced substantially. The amount of sulfur has been reduced from 550 p.p.m. to 25 p.p.m.
  • Example 1 is repeated with the exception that the solution is cooled to 0 C. instead of 24 C. About 54.5 parts of tall oil rosin crystals are obtained which contain about p.p.m. sulfur.
  • Example 1 is repeated with the exception that the solution is cooled to a temperature of about -l7 C. instead of 24 C. About 62.2 parts of crystals are obtained which contain about 60 p.p.m. sulfur.
  • Example 1 is repeated with the exception that ethyl acetate is employed in place of the acetone of Example 1 and the resulting solution is cooled to a temperature of about -17 C. instead of 24 C. About 63.1 parts of crystals are obtained which contain about p.p.m. sulfur.
  • Example 1 is repeated with the exception that methyl ethyl ketone is employed in place of acetone. About 28.7 parts of crystals are obtained which contain about 50 p.p.m. sulfur.
  • the above examples illustrate a single crystallization ethyl ether, diethylene glycol dimethyl ether, Z-methoxystep.
  • the sulfur content of the recovered crystals can be ethanol, and mixtures of two or more. further reduced if desired by repeating the crystallization 3.
  • the method of claim 1 wherein the recovered crystals procedure using the same or different solvent. The followare washed in an organic polar solvent and subsequently ing example is illustrative of a recrystallization. dried.
  • EXAMPLE 21 4. The method of clalm 2 whereln the recovered crystals are washed 1n an organic polar solvent and subse- About 50 parts of the crystals of Example 1 are dlsquently dried. solved in 50 parts of acetone to provide a solution having 5 Th h d of l i 1 h i h steps (b), a 50% solids content. The solution is cooled to about 25 nd r repeated t least once. C. and crystals are formed. The crystals, about 25 parts, 6 Th th d f 1 i 2 h r in th steps (b), are recovered by filtration and washed twice with 10 d are repeated t l t once, parts of acetone (at 0 C.).
  • the washed crystals contain from about 5 to 10 p.p.m. combined sulfur.
  • References Cited rgflfiaiii lfi f $333231?iilfii iificifir fili it: UNITED STATES PATENTS tall oil rosin of this invention can be hydrogenated g g 11/1950 Chistendon 26O 97-7 economically.
  • the hydrogenated product can be used in 547,20 4/1951 Hasselstrom the manufacture of adhesives 2,565,484 8/1951 Dunlap et al.
  • a content of sulfur not in excess of about 100 parts per million parts of tall oi l rosin which consists essentially of DONALD CZAJA, Primary Examiner (a) dlSSOlVlIlg, by weight, from about 25 parts to about 67 parts of tall oil rosin containing less than about 10% W. E. PARKER, Assistant Examiner by weight of tall oil fatty acids and sulfur-containing compounds, the amount of sulfur present therein being from about 300 to 600 parts per million parts of tall oil rosin in about parts by weight to about 33 parts by weight 0

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

DISCLOSED IS A PROCESS FOR REMOVING SULFUR COMPOUND IMPURITIES FROM TALL OIL ROSIN BY DISSOLVING TALL OIL ROSIN IN A SOLVENT FOLLOWED BY CRYSTALLIZATION OF THE ROSIN COMPONENT OF THE RESULTING SOLUTION.

Description

United States Patent Oihce Int. Cl. C09f 1/02 US. Cl. 26097.7 6 Claims ABSTRACT OF THE DISCLOSURE Disclosed is a process for removing sulfur compound impurities from tall oil rosin by dissolving tall oil rosin in a solvent followed by crystallization of the rosin component of the resulting solution.
This invention relates to tall oil rosin containing relatively small amounts of sulfur compound impurities and tothe method of obtaining same.
Tall oil, a by-product recovered from pine wood black liquor of the sulfate paper process, is comprised of rosin acids, fatty acids, certain amounts of unsaponifiable material, and trace amounts of sulfur-containing compounds. A representative tall oil rosin is one comprised of, by weight, about 43% rosin acids (also referred to in the art as resin acids), about 41% fatty acids, about 16% unsaponifiable material and trace amounts of sulfur-containing compounds. Fractional distillation of tall oil yields a fraction rich in fatty acids, and a fraction rich in rosin acids. The fraction rich in rosin acids is often referred to in the art as tall oil rosin, and will contain small amounts of fatty acids and trace amounts of sulfur-containing compounds. Further refinement of the tall oil rosin by distillation will lower the fatty acid content; however, the content of sulfur-containing compounds will remain substantially the same. The amount of sulfur present in the sulfur-containing compounds will usually be, by weight, at least about 300 parts per million (p.p.m.) parts of tall oil rosin and higher. The presence of such amounts of sulfur renders the attempted hydrogenation of tall oil rosin uneconomical in that the sulfur poisons hydrogenation catalysts, such as the noble metals, and renders them ineffective for their intended purpose.
Broadly, in accordance with this invention, there is provided a method of obtaining tall oil rosin having a content of sulfur of about 100 p.p.m. and less. It is understood that the sulfur is chemically combined and not in elemental form.
The tall oil rosin employed in carrying out this invention will be comprised of fatty acids and sulfur-containing compounds, the amount of sulfur present therein being from about 300 to about 600 parts per million (p.p.m.) parts of tall oil rosin. The fatty acids content will be less than about 10% by weight.
-In carrying out this invention, a solution is prepared by dissolving, by weight, from about 25 parts to about 67 parts of the tall oil rosin in about 75 parts to about 33 parts of a polar solvent. If required, the solvent can be heated to accomplish substantially complete dissolution of the tall oil rosin. The solution is subsequently cooled at least to a temperature at which the rosin acids will crystallize out. Crystallization is permitted to continue until the desired amount of rosin acids has precipitated. The crystals can be recovered in any convenient Patented Apr. 11, 1972 manner as by decantation, centrifugation, filtration, or the like. The recovered crystals can be washed to remove adhering impurities, if desired. Polar solvents, such as those specifically disclosed herein, are recommended for the washing step.
The polar solvent employed will be liquid under room temperature conditions. Polar solvents that are liquid at temperatures as low as about -40 C. can be satisfactorily employed. Suitable polar solvents for use in carrying out this invention include acetone, methyl ethyl ketone, ethyl acetate, ethyl alcohol, methyl isobutyl ketone, isopropyl alcohol, diethylene glycol diethyl ether (diethyl Carbitol), diethylene glycol dimethyl ether (dimethyl Carbitol), and Z-methoxyethanol (methyl Cellosolve). Mixtures of two or more polar solvents can be employed if desired.
The following examples are illustrative of this invention. All parts and percentages are by weight unless otherwise specified.
EXAMPLE 1 Tall oil rosin, 100 parts, having a fatty acid content of about 4% and containing sulfur-containing compounds, the amount of sulfur present therein being about 550 parts per million (p.p.m.) parts of tall oil rosin is dissolved in an excess amount of acetone which has been heated to its boiling point (about 565 C.) and the acetone distilled off until there is provided a solution having a solids content of about 50% The solution is cooled to a temperature of about 24 C. with constant stirring and crystals are formed. The crystals are recovered by filtration. The recovered crystals are washed with about 32 parts of cold acetone (about 0 C.) and then again washed with about 32 parts of cold acetone (about 0 C.). The Washed crystals are placed in an oven maintained at a temperature of about C. and dried. About 41.5 parts of tall oil rosin crystals are obtained which still contain trace amounts of sulfur-containing compounds; however, the amount thereof has been reduced substantially. The amount of sulfur has been reduced from 550 p.p.m. to 25 p.p.m.
EXAMPLE 2 Example 1 is repeated with the exception that the solution is cooled to 0 C. instead of 24 C. About 54.5 parts of tall oil rosin crystals are obtained which contain about p.p.m. sulfur.
EXAMPLE 3 Example 1 is repeated with the exception that the solution is cooled to a temperature of about -l7 C. instead of 24 C. About 62.2 parts of crystals are obtained which contain about 60 p.p.m. sulfur.
EXAMPLE 4 Example 1 is repeated with the exception that ethyl acetate is employed in place of the acetone of Example 1 and the resulting solution is cooled to a temperature of about -17 C. instead of 24 C. About 63.1 parts of crystals are obtained which contain about p.p.m. sulfur.
EXAMPLE 5 Example 1 is repeated with the exception that methyl ethyl ketone is employed in place of acetone. About 28.7 parts of crystals are obtained which contain about 50 p.p.m. sulfur.
The examples set forth in Table I below are in further illustration of this invention. Parts and percentages are by weight. In the Table I examples, the tall oil rosin employed has an acid number of 177.5 and is comprised of,
4 of an organic polar solvent to provide a solution, (b) cooling the solution at least to a temperature at which crystals of rosin acid form, and (c) recovering the crystals of rosin acid.
by weight, about 91.4% rosin acids; about 4.2% by weight 5 2. The method of claim 1 wherein the polar solvent fatty acids, and trace amounts of sulfur-containing comemployed is selected from the group consisting of acetone, pounds, the amount of sulfur present therein being about methyl ethyl ketone, ethyl acetate, ethyl alcohol, methyl 520 p.p.m. isobutyl ketone, isopropyl alcohol, diethylene glycol di- TABLE 1 Percent Crystalsolids lization in tempera- Example Parts, Rosin soluture, Crystals Sulfur Number Solvent solvent (parts) tion 0. (parts) (p.p.m.) Remarks 6 Mehtyl ethyl ketone... 100 100 50 25 28.7 60 Crystals washed with about parts of cold solvent (0 0.). 7.. Ethyl alcohol.. 100 100 50 33.9 64 Do. 8.. Ethyl acetate. 100 100 50 25 29. 5 72 Do. 9.. Acetone 100 100 50 25 33.0 40 Do. 10. ..do 200 200 50 0-3 100.0 52 Washed twice with 32 parts solvent. 11 Methyl ethyl kctone 200 200 50 0-3 79.9 72 Do. 12- alcohol 200 200 50 0-3 94. 5 76 D0. 13. e 100 200 66. 6 0-3 118.0 28 Do. 14. Methyl ethyl keto 100 200 66. 6 03 103. o 24 Do. 15. Ethyl alcohol 100 200 66. 6 0-3 113. 3 48 Do. 16- Ethyl acetate 100 200 66.6 0-3 115.6 24 Do. 17... Acetone 100 200 66. 6 25 100.8 56 Washed with about 120 parts aeotonltl'llc. 1s... Ethyl alcohol 100 200 66.6 25 101.3 52 Do. 19--. Ethyl acetate 300 600 66.6 0-3 343.0 80 watslllleil thtrete times with about 18 parts of B 2.08 a e. 20 Acetone 300 600 66.6 03 386.0 100 Wasbbd three times with about 65 parts cold (0 C.) solvent.
The above examples illustrate a single crystallization ethyl ether, diethylene glycol dimethyl ether, Z-methoxystep. The sulfur content of the recovered crystals can be ethanol, and mixtures of two or more. further reduced if desired by repeating the crystallization 3. The method of claim 1 wherein the recovered crystals procedure using the same or different solvent. The followare washed in an organic polar solvent and subsequently ing example is illustrative of a recrystallization. dried.
EXAMPLE 21 4. The method of clalm 2 whereln the recovered crystals are washed 1n an organic polar solvent and subse- About 50 parts of the crystals of Example 1 are dlsquently dried. solved in 50 parts of acetone to provide a solution having 5 Th h d of l i 1 h i h steps (b), a 50% solids content. The solution is cooled to about 25 nd r repeated t least once. C. and crystals are formed. The crystals, about 25 parts, 6 Th th d f 1 i 2 h r in th steps (b), are recovered by filtration and washed twice with 10 d are repeated t l t once, parts of acetone (at 0 C.). The washed crystals contain from about 5 to 10 p.p.m. combined sulfur. References Cited rgflfiaiii lfi f $333231?iilfii iificifir fili it: UNITED STATES PATENTS tall oil rosin of this invention can be hydrogenated g g 11/1950 Chistendon 26O 97-7 economically. The hydrogenated product can be used in 547,20 4/1951 Hasselstrom the manufacture of adhesives 2,565,484 8/1951 Dunlap et al. 260--97.7 It is to be understood that the above description and 3,489,740 1/1970 cholet et 260 97-7 examples are illustrative of this invention and not in limita- OTHER REFERENCES tion thereof. 6; What I claim and desire to protect by Letters Patent is: gg g g fg' and Chemlcal Engmeermg 1. A method for producing tall oil rosin containing less n 11 than about 10% by weight of tall oil fatty acids and having Hams Encyclopedla 0f chemcal Technlgy 1953 p. 781. a content of sulfur not in excess of about 100 parts per million parts of tall oi l rosin which consists essentially of DONALD CZAJA, Primary Examiner (a) dlSSOlVlIlg, by weight, from about 25 parts to about 67 parts of tall oil rosin containing less than about 10% W. E. PARKER, Assistant Examiner by weight of tall oil fatty acids and sulfur-containing compounds, the amount of sulfur present therein being from about 300 to 600 parts per million parts of tall oil rosin in about parts by weight to about 33 parts by weight 0
US794762*A 1969-01-28 1969-01-28 Tall oil rosin of low sulfur content Expired - Lifetime US3655635A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3859270A (en) * 1972-02-22 1975-01-07 Azs Corp Refining of fatty acids
US4256628A (en) * 1980-01-17 1981-03-17 Champion International Corporation Sulfur-free acidulation of tall oil soap
US4507228A (en) * 1983-03-15 1985-03-26 Westvaco Corporation Partial hydrogenation of tall oil rosin
EP2749614A1 (en) 2012-12-25 2014-07-02 Arizona Chemical Company, LLC Method for purification of rosin

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3859270A (en) * 1972-02-22 1975-01-07 Azs Corp Refining of fatty acids
US4256628A (en) * 1980-01-17 1981-03-17 Champion International Corporation Sulfur-free acidulation of tall oil soap
US4507228A (en) * 1983-03-15 1985-03-26 Westvaco Corporation Partial hydrogenation of tall oil rosin
EP2749614A1 (en) 2012-12-25 2014-07-02 Arizona Chemical Company, LLC Method for purification of rosin
WO2014102168A1 (en) 2012-12-25 2014-07-03 Arizona Chemical Company, Llc Method for purification of rosin
RU2543163C2 (en) * 2012-12-25 2015-02-27 Аризона Кемикал Кампани, ЛЛК Method of rosin purification
US20160194523A1 (en) * 2012-12-25 2016-07-07 Arizona Chemical Company, Llc Method for purification of rosin
US9828526B2 (en) * 2012-12-25 2017-11-28 Kraton Chemical, Llc Method for purification of rosin

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